EP0868423B1 - Method for the synthesis of a benzimidazole compound - Google Patents
Method for the synthesis of a benzimidazole compound Download PDFInfo
- Publication number
- EP0868423B1 EP0868423B1 EP96942702A EP96942702A EP0868423B1 EP 0868423 B1 EP0868423 B1 EP 0868423B1 EP 96942702 A EP96942702 A EP 96942702A EP 96942702 A EP96942702 A EP 96942702A EP 0868423 B1 EP0868423 B1 EP 0868423B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- process according
- carried out
- omeprazole
- methoxy
- solvent
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- PSEPRWKZZJWRCB-UHFFFAOYSA-N Cc1cnc(CO)c(C)c1OC Chemical compound Cc1cnc(CO)c(C)c1OC PSEPRWKZZJWRCB-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D401/00—Heterocyclic compounds containing two or more hetero rings, having nitrogen atoms as the only ring hetero atoms, at least one ring being a six-membered ring with only one nitrogen atom
- C07D401/02—Heterocyclic compounds containing two or more hetero rings, having nitrogen atoms as the only ring hetero atoms, at least one ring being a six-membered ring with only one nitrogen atom containing two hetero rings
- C07D401/12—Heterocyclic compounds containing two or more hetero rings, having nitrogen atoms as the only ring hetero atoms, at least one ring being a six-membered ring with only one nitrogen atom containing two hetero rings linked by a chain containing hetero atoms as chain links
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P1/00—Drugs for disorders of the alimentary tract or the digestive system
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P1/00—Drugs for disorders of the alimentary tract or the digestive system
- A61P1/04—Drugs for disorders of the alimentary tract or the digestive system for ulcers, gastritis or reflux esophagitis, e.g. antacids, inhibitors of acid secretion, mucosal protectants
Definitions
- the present invention relates to a novel process for the synthesis of 5-methoxy-2-[[(4-methoxy-3,5-dimethyl-2-pyridinyl)-methyl]sulphinyl]-1 H -benzimidazole, known under the generic name omeprazole.
- Omeprazole is an inhibitor of gastric acid secretion making it useful as an antiulcer agent.
- US 4 255 431 discloses a process for the preparation of this class of substituted benzimidazoles. Said process comprises a couple of reaction steps. The three last steps of the process utilize more than one solvent and requires isolation of intermediates to give the final product omeprazole. The resulting product is contaminated with starting materials and by-products.
- WO 91/18895 describes an improved process for synthesis of omeprazole.
- This process describes the oxidation step and a work-up procedure of omeprazole.
- the oxidation step utilizes m-chloroperoxybenzoic acid in a methylene chloride/water system at substantially constant pH of about 8.0 to 8.6.
- the work-up procedure includes crystallization of omeprazole by the addition of an alkyl formate.
- One object of the present invention is to provide a process for the manufacture of omeprazole with all three reaction steps, described above, being carried out without any isolation or purification of the intermediates, and carried out in one main solvent system common for the whole sequence.
- Such a process eliminates time consuming steps for isolation or purification of intermediates or solvent change in the process and thus making the process more efficient with a high production capacity.
- a further important benefit of such a process is that the handling of toxicological and suspected mutagenic intermediates such as pyrmethyl chloride , due to isolation or purification, is eliminated.
- Another preferred object of the present invention is to provide a process utilizing a solvent system which is environmentally friendly to avoid outlet of harmful solvents.
- a solvent system which is environmentally friendly to avoid outlet of harmful solvents.
- the novel process of the present invention gives omeprazole in a high purity without any isolation or purification of intermediates.
- the omeprazole obtained may optionally be further processed in a purification step and/or optionally processed into pharmaceutically acceptable salts.
- Another object of the present invention is to provide a process for an optional purification step of omeprazole.
- the present reaction sequence starting from pyrmethyl alcohol via pyrmethyl chloride and pyrmetazole giving omeprazole can be carried out in a main solvent system used through the whole reaction sequence.
- the solvent system is preferably inert against all reactants and suitable for the three process steps.
- step 1 pyrmethyl alcohol is reacted with an excess of thionyl chloride or another suitable chlorinating agent giving alkyl chlorides, i.e. pyrmethyl chloride.
- the reaction is preferably carried out at ambient temperature and for approximately a period of 30 minutes. The reaction may also be performed at a temperature of -5°C to 25°C.
- the reaction is carried out in a solvent system, which is used throughout the whole reaction sequence described in scheme I, i.e. from pyrmethyl alcohol to omeprazole.
- a solvent system suitable for the present process comprises a main solvent and optionally one or more co-solvents.
- the main solvent is preferably water immiscible, e.g. carbon tetrachloride, 1,1,2-trichloroethane, chloroform, methylene chloride or toluene. Toluene is especially preferred from an environmental point of view.
- the solvent system may optionally comprise co-solvent(s) to further improve/enhance the solubility of the reactants or products during the whole reaction sequence.
- the solvent system will function without any addition of a co-solvent, but the addition of such a co-solvent will enhance the process capacity, i.e. the yield per volume.
- Preferred co-solvents are alcohols and especially a lower alcohol comprising 1 - 4 carbon atoms, which carbon chain may be branched or straight.
- solvent systems include, but are not limited to, 70-80% (by volume) methylene chloride or toluene and 20-30% (by volume) lower alcohol, e . g . ethanol.
- step 2 the pyrmethyl chloride formed in step 1 is reacted with metmercazole under alkaline conditions, e.g. an alkaline aqueous solution of metmercazole is prepared and mixed with the pyrmethyl chloride in the presence of a phase transfer catalyst.
- the reaction is preferably carried out at a temperature of 30 - 60°C during a prolonged period of time.
- phase transfer catalyst may be used, for instance a tertiary amine, preferably tetrabutylammonium bromide.
- the two phases formed are separated and the aqueous phase may be extracted with the used water immiscible organic solvent, such as methylene chloride or toluene. Furthermore, an alcohol may be added to the pyrmetazole solution to improve the solubility of the formed intermediate, pyrmetazole.
- the used water immiscible organic solvent such as methylene chloride or toluene.
- an alcohol may be added to the pyrmetazole solution to improve the solubility of the formed intermediate, pyrmetazole.
- step 3 m-chloroperoxybenzoic acid is dissolved in a water immiscible organic solvent such as methylene chloride or to luene.
- a water immiscible organic solvent such as methylene chloride or to luene.
- the m-chloroperoxybenzoic acid is charged to the obtained pyrmetazole in a buffered two phase system, consisting of the water immiscible solvent, such as methylene chloride or toluene, and aqueous base, such as sodium or potassium hydrogencarbonate.
- the organic solvent may optionally be diluted with an alcohol to enhance the solubility of the m-chloroperoxybenzoic acid.
- the oxidation with m-chloroperoxybenzoic acid is preferably performed between 0°and 25°C.
- the obtained product is extracted into an alkaline, aqueous phase and the formed product is precipitated from the aqueous phase by lowering the pH of the solution to approximately 9 at ambient temperature.
- Omeprazole is isolated and washed.
- the overall yield in the process is usually higher than 75%.
- the additional purification can be carried out by crystallization from one or several organic solvents, or by precipitation from alkaline water by lowering the pH through addition of an acid or an alkyl formate.
- Suitable acids include, but are not limited to, carboxylic acids such as formic acid, acetic acid, or citric acid, and mineral acids, such as hydrogen chloride, hydrogen bromide, hydrogen fluoride, hydrogen iodide, sulfuric acid, nitric acid, or phosphoric acid.
- Preferred acids are carboxylic acids.
- Suitable alkyl formats include, but are not limited to, methyl formate and ethyl formate.
- a preferred alkyl formate is methyl formate.
- Omeprazole was precipitated from the aqueous phase by the addition of 12 mL methyl formate, filtered and washed with water/methanol and dried. Omeprazole was obtained in a yield of 76%.
- the formed pyrmethyl chloride in toluene was mixed with an alkaline aqueous solution of 18.0 g (0.10 mol) metmercazole.
- the reaction was performed in the presence of 0.9 g tetrabutylammonium bromide at 40°C during a couple of hours.
- the two phases were separated and the aqueous phase was extracted with toluene. Ethanol was added to improve the solubility of the resulting product before the solution was cooled to ambient temperature.
- the product was dissolved at an alkaline pH by addition of sodium hydroxide. The solution was filtered and cooled to approximately 0°C.
- omeprazole prepared according to example 1, 69 mL of methanol, 34 mL of methylene chloride and 0.3 mL of ammonia were mixed at ambient temperature and the obtained solution was filtered.
- the product was precipitated by evaporation of methylene chloride under reduced pressure.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Medicinal Chemistry (AREA)
- Nuclear Medicine, Radiotherapy & Molecular Imaging (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Pharmacology & Pharmacy (AREA)
- Engineering & Computer Science (AREA)
- Animal Behavior & Ethology (AREA)
- General Health & Medical Sciences (AREA)
- Public Health (AREA)
- Veterinary Medicine (AREA)
- Plural Heterocyclic Compounds (AREA)
- Nitrogen Condensed Heterocyclic Rings (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
Abstract
Description
- The present invention relates to a novel process for the synthesis of 5-methoxy-2-[[(4-methoxy-3,5-dimethyl-2-pyridinyl)-methyl]sulphinyl]-1H-benzimidazole, known under the generic name omeprazole.
- Omeprazole is an inhibitor of gastric acid secretion making it useful as an antiulcer agent. US 4 255 431 (corresponding to EP 0 005 129) discloses a process for the preparation of this class of substituted benzimidazoles. Said process comprises a couple of reaction steps. The three last steps of the process utilize more than one solvent and requires isolation of intermediates to give the final product omeprazole. The resulting product is contaminated with starting materials and by-products.
- WO 91/18895 describes an improved process for synthesis of omeprazole. This process describes the oxidation step and a work-up procedure of omeprazole. The oxidation step utilizes m-chloroperoxybenzoic acid in a methylene chloride/water system at substantially constant pH of about 8.0 to 8.6. The work-up procedure includes crystallization of omeprazole by the addition of an alkyl formate.
- Another process for the manufacture of omeprazole is described in US 5 391 752. This process also describes only the oxidation step. Said oxidation step utilizes magnesium monoperoxyphtalate as an oxidizing agent. The resulting product is contaminated with starting material and by-products.
- Yet another process for the manufacture of compounds showing structural similarities to omeprazole is disclosed in US 4 619 997. The intermediates are isolated, but not purified, and different solvent systems are used in the chemical steps throughout the process.
- In the light of the above there was still a need for a new convenient and more efficient process to manufacture omeprazole.
- In the following the improved process is described. Scheme I below describes three main reaction sequences in the manufacture of omeprazole. In the scheme the complete chemical names as well as short names for the starting material and the different intermediates are stated. The starting material as well as the reactants used are readily available by procedures described in the literature.
- Step 1:
- Step 2:
- Step 3:
-
- Advantages of the improved process of the present invention are disclosed in the following paragraphs.
- One object of the present invention is to provide a process for the manufacture of omeprazole with all three reaction steps, described above, being carried out without any isolation or purification of the intermediates, and carried out in one main solvent system common for the whole sequence. Such a process eliminates time consuming steps for isolation or purification of intermediates or solvent change in the process and thus making the process more efficient with a high production capacity. A further important benefit of such a process is that the handling of toxicological and suspected mutagenic intermediates such as pyrmethyl chloride , due to isolation or purification, is eliminated.
- Another preferred object of the present invention is to provide a process utilizing a solvent system which is environmentally friendly to avoid outlet of harmful solvents. There is a general interest from environmental groups both inside and outside the pharmaceutical industry that the industry shall develop and use environmentally friendly processes. In some countries the authorities also have made restrictions on the outlet of harmful chlorinated solvents into the air.
- Surprisingly, the novel process of the present invention gives omeprazole in a high purity without any isolation or purification of intermediates. The omeprazole obtained may optionally be further processed in a purification step and/or optionally processed into pharmaceutically acceptable salts.
- Another object of the present invention is to provide a process for an optional purification step of omeprazole.
- Further, the present reaction sequence starting from pyrmethyl alcohol via pyrmethyl chloride and pyrmetazole giving omeprazole can be carried out in a main solvent system used through the whole reaction sequence. The solvent system is preferably inert against all reactants and suitable for the three process steps.
- In step 1 pyrmethyl alcohol is reacted with an excess of thionyl chloride or another suitable chlorinating agent giving alkyl chlorides, i.e. pyrmethyl chloride. The reaction is preferably carried out at ambient temperature and for approximately a period of 30 minutes. The reaction may also be performed at a temperature of -5°C to 25°C.
- The reaction is carried out in a solvent system, which is used throughout the whole reaction sequence described in scheme I, i.e. from pyrmethyl alcohol to omeprazole. Such a solvent system suitable for the present process comprises a main solvent and optionally one or more co-solvents. The main solvent is preferably water immiscible, e.g. carbon tetrachloride, 1,1,2-trichloroethane, chloroform, methylene chloride or toluene. Toluene is especially preferred from an environmental point of view.
- Furthermore, the solvent system may optionally comprise co-solvent(s) to further improve/enhance the solubility of the reactants or products during the whole reaction sequence. The solvent system will function without any addition of a co-solvent, but the addition of such a co-solvent will enhance the process capacity, i.e. the yield per volume. Preferred co-solvents are alcohols and especially a lower alcohol comprising 1 - 4 carbon atoms, which carbon chain may be branched or straight.
- Examples of solvent systems include, but are not limited to, 70-80% (by volume) methylene chloride or toluene and 20-30% (by volume) lower alcohol, e.g. ethanol.
- In step 2, the pyrmethyl chloride formed in step 1 is reacted with metmercazole under alkaline conditions, e.g. an alkaline aqueous solution of metmercazole is prepared and mixed with the pyrmethyl chloride in the presence of a phase transfer catalyst. The reaction is preferably carried out at a temperature of 30 - 60°C during a prolonged period of time.
- Metmercazole is charged in approximately stoichiometric amount to the pyrmethyl chloride. A phase transfer catalyst may be used, for instance a tertiary amine, preferably tetrabutylammonium bromide.
- The two phases formed are separated and the aqueous phase may be extracted with the used water immiscible organic solvent, such as methylene chloride or toluene. Furthermore, an alcohol may be added to the pyrmetazole solution to improve the solubility of the formed intermediate, pyrmetazole.
- In step 3, m-chloroperoxybenzoic acid is dissolved in a water immiscible organic solvent such as methylene chloride or to luene. The m-chloroperoxybenzoic acid is charged to the obtained pyrmetazole in a buffered two phase system, consisting of the water immiscible solvent, such as methylene chloride or toluene, and aqueous base, such as sodium or potassium hydrogencarbonate. The organic solvent may optionally be diluted with an alcohol to enhance the solubility of the m-chloroperoxybenzoic acid. The oxidation with m-chloroperoxybenzoic acid is preferably performed between 0°and 25°C. The obtained product is extracted into an alkaline, aqueous phase and the formed product is precipitated from the aqueous phase by lowering the pH of the solution to approximately 9 at ambient temperature. Omeprazole is isolated and washed. The overall yield in the process is usually higher than 75%.
- The additional purification can be carried out by crystallization from one or several organic solvents, or by precipitation from alkaline water by lowering the pH through addition of an acid or an alkyl formate.
- Examples of suitable acids include, but are not limited to, carboxylic acids such as formic acid, acetic acid, or citric acid, and mineral acids, such as hydrogen chloride, hydrogen bromide, hydrogen fluoride, hydrogen iodide, sulfuric acid, nitric acid, or phosphoric acid. Preferred acids are carboxylic acids. Suitable alkyl formats include, but are not limited to, methyl formate and ethyl formate. A preferred alkyl formate is methyl formate.
- The present invention is described more in detail in the following non-limiting examples.
- 17.8 g (0.15 mol) Thionyl chloride in 13 mL methylene chloride was charged to a methylene chloride solution of 16.8 g (0.10 mol) pyrmethyl alcohol at ambient temperature. The solution was stirred for approximately 30 minutes.
- 18.0 g (0.10 mol) Metmercazole, 47.3 g (0.58 mol) aqueous sodium hydroxide (50% w/w) and tetrabutylammonium bromide (0.9 g) were mixed at ambient temperature. The pyrmethyl chloride solution was added at a temperature between 25° - 40°C and the mixture was refluxed for 1 - 2 hours. The two phases were separated and the aqueous phase was washed with methylene chloride. The organic phases were combined.
- 10.4 g (0.10 mol) Potassium bicarbonate dissolved in water was added to the pyrmetazole solution.
- 22.3 g (0.099 mol) Meta-chloroperoxybenzoic acid (76.5% w/w) dissolved in 42 mL of methylene chloride and 10 mL of ethanol were charged to the prepared mixture of pyrmetazole in methylene chloride and potassium bicarbonate in water. The oxidation was carried out at 0 - 15°C. The product was extracted into the aqueous phase at an alkaline pH by addition of sodium hydroxide. The two phases were separated and the organic phase was washed with an alkaline water solution. The aqueous phases were combined.
- Omeprazole was precipitated from the aqueous phase by the addition of 12 mL methyl formate, filtered and washed with water/methanol and dried. Omeprazole was obtained in a yield of 76%.
- 13.1 g (0.11 mol) Thionyl chloride was charged to a toluene solution of 16.7 g (0.10 mol) pyrmethyl alcohol at ambient temperature. The reaction was continued for approximately 30 minutes.
- The formed pyrmethyl chloride in toluene was mixed with an alkaline aqueous solution of 18.0 g (0.10 mol) metmercazole. The reaction was performed in the presence of 0.9 g tetrabutylammonium bromide at 40°C during a couple of hours. The two phases were separated and the aqueous phase was extracted with toluene. Ethanol was added to improve the solubility of the resulting product before the solution was cooled to ambient temperature.
- 24.4 g (0.10 mol) Meta-chloroperoxybenzoic acid in 42 mL toluene and 10 mL ethanol were charged to a two phase system prepared from the obtained pyrmetazole toluene solution, and potassium bicarbonate (13.8 g) in water (120 mL). The oxidation was performed between 0°C and room temperature. The product was extracted into an alkaline aqueous phase by the addition of sodium hydroxide. The two phases were separated and the organic phase was washed with water. Omeprazole was precipitated by lowering the pH of the solution to approximately 9 at ambient temperature. Omeprazole was isolated, washed, and dried. The overall yield was approximately 77%.
- 20.0 g (0.0579 mol) of omeprazole, prepared according to example 1, 125 mL of methanol and 54 mL of water were mixed at ambient temperature.
- The product was dissolved at an alkaline pH by addition of sodium hydroxide. The solution was filtered and cooled to approximately 0°C.
- The product was precipitated by addition of diluted acetic acid, filtered and washed with water/methanol, and thereafter dried. Omeprazole was obtained in a yield of 90 %.
- 11.2 g (0.0324 mol) of omeprazole, prepared according to example 1, 69 mL of methanol, 34 mL of methylene chloride and 0.3 mL of ammonia were mixed at ambient temperature and the obtained solution was filtered.
- The product was precipitated by evaporation of methylene chloride under reduced pressure.
- 0.3 mL of ammonia was added and the slurry was cooled to 0°C.
- The product was filtered, washed with methanol containing approximately 1% v/v of ammonia, and dried. Omeprazole was obtained in a yield of 90 %.
- With respect to the environmental point of view, the best way to carry out one aspect of the present invention is according to the process described in Example 2.
Claims (12)
- A process for the manufacture of 5-methoxy-2-[[(4-methoxy-3,5-dimethyl-2-pyridinyl)-methyl]sulphinyl]-1H-benzimidazole from (4-methoxy-3,5-dimethyl-2-pyridinyl)-methyl alcohol comprising the following reaction steps
- A process according to claim 1, characterized in that the solvent system comprises a main solvent and optionally one or more co-solvents.
- A process according to claim 2, characterized in that the main solvent is methylene chloride.
- A process according to claim 2, characterized in that the main solvent is toluene.
- A process according to claim 2, characterized in that the co-solvent is an alcohol.
- A process according to claim 1, characterized in that step 1 is carried out at a temperature between -5°C to 25°C.
- A process according to clam 1, characterized in that step 2 is carried out with a phase transfer catalyst.
- A process according to claim 7, characterized in that the phase transfer catalyst is tetrabutylammonium bromide.
- A process according to claim 1, characterized in that step 2 is carried out at a temperature between 30°C to 60°C.
- A process according to anyone of the preceeding claims wherein the resulting 5-methoxy-2-[[(4-methoxy-3,5-dimethyl-2-pyridinyl)-methyl]sulphinyl]-1H-benzimidazole is further purified in a purification step.
- A process according to claim 10, characterized in that the purification step involves crystallization from one or several organic solvents.
- A process according to claim 10, characterized in that the purification step involves precipitation from alkaline water by lowering the pH through addition of an acid or an alkyl formate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SI9630367T SI0868423T1 (en) | 1995-12-15 | 1996-12-05 | Method for the synthesis of a benzimidazole compound |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE9504503A SE521100C2 (en) | 1995-12-15 | 1995-12-15 | Process for the preparation of a benzimidazole compound |
SE9504503 | 1995-12-15 | ||
PCT/SE1996/001603 WO1997022603A1 (en) | 1995-12-15 | 1996-12-05 | Method for the synthesis of a benzimidazole compound |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0868423A1 EP0868423A1 (en) | 1998-10-07 |
EP0868423B1 true EP0868423B1 (en) | 2001-09-05 |
Family
ID=20400614
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP96942702A Expired - Lifetime EP0868423B1 (en) | 1995-12-15 | 1996-12-05 | Method for the synthesis of a benzimidazole compound |
Country Status (40)
Country | Link |
---|---|
US (1) | US5958955A (en) |
EP (1) | EP0868423B1 (en) |
JP (1) | JP3523267B2 (en) |
KR (1) | KR100433436B1 (en) |
CN (1) | CN1113879C (en) |
AR (1) | AR004834A1 (en) |
AT (1) | ATE205201T1 (en) |
AU (1) | AU704422B2 (en) |
CA (1) | CA2238864C (en) |
CO (1) | CO4750654A1 (en) |
CZ (1) | CZ288661B6 (en) |
DE (2) | DE868423T1 (en) |
DK (1) | DK0868423T3 (en) |
DZ (1) | DZ2137A1 (en) |
EE (1) | EE03768B1 (en) |
EG (1) | EG23859A (en) |
ES (1) | ES2125210T3 (en) |
HK (1) | HK1010539A1 (en) |
HR (1) | HRP960581B1 (en) |
HU (1) | HUP9900110A3 (en) |
IL (1) | IL124856A (en) |
IS (1) | IS1891B (en) |
MA (1) | MA24026A1 (en) |
MX (1) | MX9804603A (en) |
MY (1) | MY115661A (en) |
NO (1) | NO314306B1 (en) |
NZ (1) | NZ324482A (en) |
PL (1) | PL186132B1 (en) |
PT (1) | PT868423E (en) |
RU (1) | RU2166502C2 (en) |
SE (1) | SE521100C2 (en) |
SI (1) | SI0868423T1 (en) |
SK (1) | SK282347B6 (en) |
TN (1) | TNSN96148A1 (en) |
TR (1) | TR199801070T2 (en) |
TW (1) | TW460474B (en) |
UA (1) | UA62921C2 (en) |
WO (1) | WO1997022603A1 (en) |
YU (1) | YU49420B (en) |
ZA (1) | ZA9610067B (en) |
Families Citing this family (24)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SE521100C2 (en) * | 1995-12-15 | 2003-09-30 | Astra Ab | Process for the preparation of a benzimidazole compound |
US6645988B2 (en) | 1996-01-04 | 2003-11-11 | Curators Of The University Of Missouri | Substituted benzimidazole dosage forms and method of using same |
US5840737A (en) | 1996-01-04 | 1998-11-24 | The Curators Of The University Of Missouri | Omeprazole solution and method for using same |
US6699885B2 (en) * | 1996-01-04 | 2004-03-02 | The Curators Of The University Of Missouri | Substituted benzimidazole dosage forms and methods of using same |
US6489346B1 (en) | 1996-01-04 | 2002-12-03 | The Curators Of The University Of Missouri | Substituted benzimidazole dosage forms and method of using same |
SK283805B6 (en) | 1996-09-09 | 2004-02-03 | Slovakofarma, A. S. | Method of omeprazole preparation |
US6303787B1 (en) * | 1998-05-27 | 2001-10-16 | Natco Pharma Limited | Intermediates and an improved process for the preparation of Omeprazole employing the said intermediates |
SI20019A (en) * | 1998-07-13 | 2000-02-29 | LEK, tovarna farmacevtskih in kemi�nih izdelkov, d.d. | An improved process for synthesis of 5-methoxy-2-/(4-methoxy-3,5-dimethyl-2-pyridyl)methyl/ sulphynyl-1h-benzimidazol |
US6166213A (en) * | 1998-08-11 | 2000-12-26 | Merck & Co., Inc. | Omeprazole process and compositions thereof |
IL142703A (en) | 1998-11-10 | 2006-04-10 | Astrazeneca Ab | Crystalline form of omeprazole |
UA72748C2 (en) * | 1998-11-10 | 2005-04-15 | Astrazeneca Ab | A novel crystalline form of omeprazole |
DE19951960C2 (en) * | 1999-10-28 | 2002-06-27 | Gruenenthal Gmbh | Process for the preparation of benzimidazole derivatives suitable as ulcer therapeutics |
US20040006111A1 (en) * | 2002-01-25 | 2004-01-08 | Kenneth Widder | Transmucosal delivery of proton pump inhibitors |
SE0203092D0 (en) * | 2002-10-18 | 2002-10-18 | Astrazeneca Ab | Method for the synthesis of a benzimidazole compound |
US8993599B2 (en) | 2003-07-18 | 2015-03-31 | Santarus, Inc. | Pharmaceutical formulations useful for inhibiting acid secretion and methods for making and using them |
US8815916B2 (en) | 2004-05-25 | 2014-08-26 | Santarus, Inc. | Pharmaceutical formulations useful for inhibiting acid secretion and methods for making and using them |
US8906940B2 (en) | 2004-05-25 | 2014-12-09 | Santarus, Inc. | Pharmaceutical formulations useful for inhibiting acid secretion and methods for making and using them |
AU2005315390B2 (en) * | 2004-12-16 | 2011-10-27 | Cipla Limited | Process for the preparation of pantoprazole sodium |
CN100393712C (en) * | 2006-01-23 | 2008-06-11 | 中国科学院成都有机化学有限公司 | Improved preparation and separated purification method of benzimidazole type proton pump inhibitors and precursor thereof |
WO2007122686A1 (en) * | 2006-04-14 | 2007-11-01 | Eisai R & D Management Co., Ltd. | Benzimidazole compounds |
CA2678702A1 (en) * | 2007-02-21 | 2008-08-28 | Cipla Limited | Process for the preparation of esomeprazole magnesium dihydrate |
CN101492459B (en) * | 2008-01-25 | 2011-04-27 | 山东轩竹医药科技有限公司 | Compound containing alcoxyl acetyl dihydrogen isoxazole-pyridine |
CN101497603B (en) * | 2008-01-30 | 2012-11-07 | 山东轩竹医药科技有限公司 | Benzimidazole derivative containing alkoxy alkanamine oxyl substituted pyridine |
CN103664885A (en) * | 2013-12-12 | 2014-03-26 | 武汉工程大学 | Preparation method of benzimidazole proton pump inhibitor intermediate |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US461997A (en) * | 1891-10-27 | Sand-pump or other pipes | ||
SE7804231L (en) * | 1978-04-14 | 1979-10-15 | Haessle Ab | Gastric acid secretion |
JPS6150978A (en) * | 1984-08-16 | 1986-03-13 | Takeda Chem Ind Ltd | Pyridine derivative and preparation thereof |
US4619997A (en) * | 1984-09-06 | 1986-10-28 | The Upjohn Company | Substituted 2-pyridylmethylthio and sulfinyl-benzimidazoles as gastric antisecretory agents |
IL76839A (en) * | 1984-10-31 | 1988-08-31 | Byk Gulden Lomberg Chem Fab | Picoline derivatives,processes for the preparation thereof and pharmaceutical compositions containing the same |
SE9002043D0 (en) * | 1990-06-07 | 1990-06-07 | Astra Ab | IMPROVED METHOD FOR SYNTHESIS |
NZ244301A (en) * | 1991-09-20 | 1994-08-26 | Merck & Co Inc | Preparation of 2-pyridylmethylsulphinylbenzimidazole and pyridoimidazole derivatives from the corresponding sulphenyl compounds |
SE521100C2 (en) * | 1995-12-15 | 2003-09-30 | Astra Ab | Process for the preparation of a benzimidazole compound |
-
1995
- 1995-12-15 SE SE9504503A patent/SE521100C2/en not_active IP Right Cessation
-
1996
- 1996-05-12 UA UA98052782A patent/UA62921C2/en unknown
- 1996-11-29 ZA ZA9610067A patent/ZA9610067B/en unknown
- 1996-12-02 AR ARP960105459A patent/AR004834A1/en active IP Right Grant
- 1996-12-02 TN TNTNSN96148A patent/TNSN96148A1/en unknown
- 1996-12-03 TW TW085114881A patent/TW460474B/en not_active IP Right Cessation
- 1996-12-04 YU YU64296A patent/YU49420B/en unknown
- 1996-12-04 DZ DZ960182A patent/DZ2137A1/en active
- 1996-12-04 MA MA24415A patent/MA24026A1/en unknown
- 1996-12-05 JP JP52269797A patent/JP3523267B2/en not_active Expired - Fee Related
- 1996-12-05 CZ CZ19981685A patent/CZ288661B6/en not_active IP Right Cessation
- 1996-12-05 IL IL12485696A patent/IL124856A/en not_active IP Right Cessation
- 1996-12-05 RU RU98110659/04A patent/RU2166502C2/en not_active IP Right Cessation
- 1996-12-05 SK SK768-98A patent/SK282347B6/en not_active IP Right Cessation
- 1996-12-05 AU AU11550/97A patent/AU704422B2/en not_active Ceased
- 1996-12-05 SI SI9630367T patent/SI0868423T1/en unknown
- 1996-12-05 ES ES96942702T patent/ES2125210T3/en not_active Expired - Lifetime
- 1996-12-05 HU HU9900110A patent/HUP9900110A3/en unknown
- 1996-12-05 WO PCT/SE1996/001603 patent/WO1997022603A1/en active IP Right Grant
- 1996-12-05 EP EP96942702A patent/EP0868423B1/en not_active Expired - Lifetime
- 1996-12-05 CA CA002238864A patent/CA2238864C/en not_active Expired - Fee Related
- 1996-12-05 DK DK96942702T patent/DK0868423T3/en active
- 1996-12-05 CN CN96199057A patent/CN1113879C/en not_active Expired - Fee Related
- 1996-12-05 PL PL96327334A patent/PL186132B1/en not_active IP Right Cessation
- 1996-12-05 DE DE0868423T patent/DE868423T1/en active Pending
- 1996-12-05 PT PT96942702T patent/PT868423E/en unknown
- 1996-12-05 NZ NZ324482A patent/NZ324482A/en unknown
- 1996-12-05 EE EE9800183A patent/EE03768B1/en not_active IP Right Cessation
- 1996-12-05 TR TR1998/01070T patent/TR199801070T2/en unknown
- 1996-12-05 AT AT96942702T patent/ATE205201T1/en not_active IP Right Cessation
- 1996-12-05 US US08/776,222 patent/US5958955A/en not_active Expired - Lifetime
- 1996-12-05 DE DE69615052T patent/DE69615052T2/en not_active Expired - Fee Related
- 1996-12-05 KR KR10-1998-0704454A patent/KR100433436B1/en not_active IP Right Cessation
- 1996-12-09 HR HR960581A patent/HRP960581B1/en not_active IP Right Cessation
- 1996-12-11 CO CO96065025A patent/CO4750654A1/en unknown
- 1996-12-13 MY MYPI96005252A patent/MY115661A/en unknown
- 1996-12-14 EG EG112296A patent/EG23859A/en active
-
1998
- 1998-05-22 IS IS4750A patent/IS1891B/en unknown
- 1998-06-08 NO NO19982624A patent/NO314306B1/en not_active IP Right Cessation
- 1998-06-09 MX MX9804603A patent/MX9804603A/en not_active IP Right Cessation
- 1998-10-29 HK HK98111601A patent/HK1010539A1/en not_active IP Right Cessation
Also Published As
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0868423B1 (en) | Method for the synthesis of a benzimidazole compound | |
CA2663981C (en) | Process for preparing trityl olmesartan medoxomil and olmesartan medoxomil | |
KR100671881B1 (en) | Process for preparation of penam derivatives from cepham derivatives | |
MXPA05003994A (en) | Method for the synthesis of a benzimidazole compound. | |
EP0323105B1 (en) | Process for the preparation of 3-methylindazole-3-carboxylic acid | |
EP1368338A1 (en) | Method of preparing lansoprazole and its intermediate | |
EP1484321B1 (en) | Process for preparing 1-methylindazole-3-carboxylic acid | |
JP3884063B2 (en) | Cefcapene pivoxil methanesulfonate | |
JP2001515496A (en) | Method for producing 5-aminomethyl-chloropyridines | |
EP0257361A2 (en) | 5-fluorouridine derivative and preparation of the same | |
EP0306936A2 (en) | Process for producing aminooxyacetic acid salts | |
WO2004041830A2 (en) | An improved process for the preparation of biotin | |
JP2010526126A (en) | Method for producing valsartan | |
JP2019135220A (en) | Manufacturing method of l-carnosine and derivative thereof | |
JPH08225572A (en) | Improved method of massproducing bms180048 and analogue | |
WO2011136510A2 (en) | Novel method for preparing losartan metabolite exp-3174 dihydrate | |
SA96170440B1 (en) | benzimidazole A process that synthesizes a benzimidazole compound | |
JPH06211796A (en) | 3-substituted quinoline-5-carboxylic acid | |
JP2002531571A (en) | Method for producing penicillanic acid sulfoxide ester | |
JPH07118219A (en) | Production of hydrazone compound |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
17P | Request for examination filed |
Effective date: 19980715 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AT BE CH DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE |
|
EL | Fr: translation of claims filed | ||
REG | Reference to a national code |
Ref country code: ES Ref legal event code: BA2A Ref document number: 2125210 Country of ref document: ES Kind code of ref document: T1 |
|
TCAT | At: translation of patent claims filed | ||
DET | De: translation of patent claims | ||
TCNL | Nl: translation of patent claims filed | ||
RAP1 | Party data changed (applicant data changed or rights of an application transferred) |
Owner name: ASTRAZENECA AB |
|
17Q | First examination report despatched |
Effective date: 20000331 |
|
GRAG | Despatch of communication of intention to grant |
Free format text: ORIGINAL CODE: EPIDOS AGRA |
|
GRAG | Despatch of communication of intention to grant |
Free format text: ORIGINAL CODE: EPIDOS AGRA |
|
GRAG | Despatch of communication of intention to grant |
Free format text: ORIGINAL CODE: EPIDOS AGRA |
|
GRAH | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOS IGRA |
|
GRAH | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOS IGRA |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AT BE CH DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE |
|
AX | Request for extension of the european patent |
Free format text: LT PAYMENT 19980715;LV PAYMENT 19980715;RO PAYMENT 19980715;SI PAYMENT 19980715 |
|
REF | Corresponds to: |
Ref document number: 205201 Country of ref document: AT Date of ref document: 20010915 Kind code of ref document: T |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: EP |
|
REF | Corresponds to: |
Ref document number: 69615052 Country of ref document: DE Date of ref document: 20011011 |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: FG4D |
|
REG | Reference to a national code |
Ref country code: DK Ref legal event code: T3 |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: IF02 |
|
ET | Fr: translation filed | ||
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FG2A Ref document number: 2125210 Country of ref document: ES Kind code of ref document: T3 |
|
REG | Reference to a national code |
Ref country code: PT Ref legal event code: SC4A Free format text: AVAILABILITY OF NATIONAL TRANSLATION Effective date: 20011113 |
|
REG | Reference to a national code |
Ref country code: GR Ref legal event code: EP Ref document number: 20010402333 Country of ref document: GR |
|
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
26N | No opposition filed | ||
REG | Reference to a national code |
Ref country code: SI Ref legal event code: IF |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: NL Payment date: 20081111 Year of fee payment: 13 Ref country code: MC Payment date: 20081104 Year of fee payment: 13 Ref country code: LU Payment date: 20081021 Year of fee payment: 13 Ref country code: IE Payment date: 20081016 Year of fee payment: 13 Ref country code: DK Payment date: 20081112 Year of fee payment: 13 Ref country code: CH Payment date: 20081028 Year of fee payment: 13 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: PT Payment date: 20081006 Year of fee payment: 13 Ref country code: FI Payment date: 20081112 Year of fee payment: 13 Ref country code: ES Payment date: 20081222 Year of fee payment: 13 Ref country code: AT Payment date: 20081110 Year of fee payment: 13 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: SE Payment date: 20081208 Year of fee payment: 13 Ref country code: IT Payment date: 20081216 Year of fee payment: 13 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 20081205 Year of fee payment: 13 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20081230 Year of fee payment: 13 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GR Payment date: 20081014 Year of fee payment: 13 Ref country code: GB Payment date: 20081110 Year of fee payment: 13 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: BE Payment date: 20090112 Year of fee payment: 13 |
|
REG | Reference to a national code |
Ref country code: PT Ref legal event code: MM4A Free format text: LAPSE DUE TO NON-PAYMENT OF FEES Effective date: 20100607 |
|
BERE | Be: lapsed |
Owner name: *ASTRAZENECA A.B. Effective date: 20091231 |
|
REG | Reference to a national code |
Ref country code: NL Ref legal event code: V1 Effective date: 20100701 |
|
EUG | Se: european patent has lapsed | ||
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: PT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20100607 Ref country code: MC Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20100701 |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
REG | Reference to a national code |
Ref country code: DK Ref legal event code: EBP |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 20091205 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FI Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20091205 Ref country code: AT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20091205 |
|
REG | Reference to a national code |
Ref country code: SI Ref legal event code: KO00 Effective date: 20100709 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: ST Effective date: 20100831 |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: MM4A |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20100701 Ref country code: LI Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20091231 Ref country code: IE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20091207 Ref country code: FR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20091231 Ref country code: CH Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20091231 Ref country code: BE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20091231 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20100701 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GB Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20091205 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DK Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20100104 |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FD2A Effective date: 20110309 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20091205 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20091205 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20091206 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: ES Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20110308 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: ES Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20091206 |